• Journal of the Korea Academia-Industrial cooperation Society
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• v.7 no.4
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• pp.727-732
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• 2006

The object of this study was to investigate the influence of composition and concentration of electrolyte, ratio of cation to anion exchange resin of mixed ion exchange column in the performance of ion exchange. Also this work examined the removal capability of suspended solids by ion exchange resin and the effect of particule on the characteristics of ion exchange. Breakthrough time was extended as the amount of ions and particles present in liquid was decreased. The case of anion, the breakthrough sequence is $Cl^{-}, but the case of cation, the breakthrough sequence is $Na^{+}. As for the ratio of cation to anion exchange resin of 1:2, the breakthrough time was prolonged compared with that of 1:1 and 1:3. For the electrolyte of equal concentration containing suspended solid, breakthrough time was contracted less than 20%. It results in the increase in the removal capacity of cation exchange resin. For the higher ratio of cation exchange resin, suspended solids are shorten the cation's breakthrough time so that the runtime of ion exchange resin tower is increased.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2003.11b
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• pp.179-180
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• 2003

자동차 도장 작업 시 배출되는 대표적인 용매물질인 부틸아세테이트, n-부탄올 및 톨루엔을 대상기체로 하여 활성탄에 의한 흡착 특성을 연구결과는 다음과 같았다. 처리대상가스의 유입농도가 증가할수록 파과시간은 점점 감소하였으며. 파과곡선의 기울기 또한 급격해졌다. 유량이 증가할수록 파과시간은 감소하였다.

• Applied Chemistry for Engineering
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• v.10 no.2
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• pp.206-211
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• 1999

Mixed-bed ion exchange performance was studied experimentally with variations of cation to anion resin ratio, resin weight and temperature at ultralow sodium chloride solution concentrations of less than $1.0{\times}10^{-4}M$. Analyzing the effluent concentration histories the performance test was examined as a function of tested solution volume for a laboratory-scale continuous flow column until both the cation and anion-exchange resins were exhausted. Initial leakage was observed for both cation and anion breakthrough curves, but serious at cation breakthrough curve because of low selectivity coefficient. The slope of breakthrough curve was affected by selectivity coefficient and temperature. The slope of anion breakthrough curve was steep because of the large selectivity coefficient, and ion exchange rates increased as temperature increased. The temperature effect decreased as the total volume was increased or as the resins were exhausted.

• Applied Chemistry for Engineering
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• v.16 no.1
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• pp.131-138
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• 2005

Freundlich isotherms and Toth isotherms were obtained for benzene adsorption on activated carbon and zeolite 13X in static experiments. Breakthrough curves of benzene were measured in adsorption bed packed with the same adsorbents. Relation between breakthrough times and partial pressure of benzene was analyzed and the Freundlich isotherm parameters were determined. Adsorption amount of benzene predicted by the analysis of breakthrough experimental results was relatively consistent with that predicted by the static experimental results. Dynamic experiments for activated carbon bed, where more symmetric breakthrough curves were obtained, produced smaller errors with zeolite bed.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2004.05a
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• pp.324-328
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• 2004

본 연구에서는 활성탄을 염화철로 표면 처리한 염화철처리 활성탄을 사용하여 지하수중의 ${NO_3}^{-}$－/-N 제거 가능성과 그 제거에 미치는 영향을 검토하고자 한 것으로 다음과 같은 결론을 얻었다. 1) 조제된 염화철 코팅 활성탄의 표면을 SEM으로 분석한 결과를 보면 활성탄의 표면에 염화철이 코팅되어 있는 것을 확인할 수 있었다. 2) 통수유속이 0.5~4 BV $hr^{-1}$/로 낮을 경우는 질산성 질소 파과시점이 비슷하였으며, 통수유속이 커질수록 활성탄의 비표면적에 접하는 시간이 짧아져서 파과시점이 짧아진 것으로 사료된다. 3) 연속컬럼 실험(3.1 L)에서 통수량 약 82 L까지는 ${NO_3}^{-}$/-N의 파과시점이 나타나지 않았으며 재생액의 농도가 0.5 M-KCl에서는 약 9 L, 1 M-KCl에서는 약 7 L의 재생액이 사용되었고, 재생 후 각각의 파과시점은 약 53 L, 59 L로 유지되었다. 1 M-KCl의 재생액을 사용하여 재생하였을 경우 두번째 재사용과 재생부터 총 질산성 질소 제거량은 약 1,531~l,357 mg/kg, 탈착량은 약 1,526~1,306 mg/kg으로 일정하였다.

• Clean Technology
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• v.10 no.3
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• pp.159-168
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• 2004

Benzene adsorption experiment was carried out for activated carbon and zeolite 13X adsorbents. Single column and dual column packed with two adsorbents were used to investigate the dynamic adsorptive characteristics. Effect of feed flow rate on the breakthrough curve was not significant. Specific adsorption amount of benzene for activated carbon was larger than that for zeolite 13X. On the contrary, adsorption amount per column volume was larger for zeolite 13X column because the density of zeolite 13X was larger. In the dynamic experiment using dual adsorbents column, length of mass transfer zone was changed by the feed direction. Breakthrough time was longer and breakthrough curve was sharper when activated carbon was packed in feed inlet and zeolite 13X was packed in column outlet. Also breakthrough time and breakthrough curve slope were affected by the packing ratio of the two adsorbents.

• Journal of Korea Water Resources Association
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• v.55 no.1
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• pp.23-32
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• 2022

This paper performs two-dimensional numerical simulation of surface water-groundwater coupled flow and solute transport to investigate the effect of the hyporheic exchange at the sediment-water interface (SWI) on surface solute transport. For the impermeable bed case in the absence of hyporheic flow, the trapping effect of flow recirculation associated with the ripple bed controls the shape of breakthrough curves (BTCs). However, the permeable bed case with hyporheic flow stimulates the extended tailing of the BTCs more significantly due to the elevated concentration of the BTC tailing resulting from slow hyporheic velocity. Also, the increased bottom pressure at the SWI with an increase in surface velocity shortens the BTC tailing because of increasing hyporheic velocity. These results infer that hyporhiec flow is critically important in predicting solute residence times in surface water.

• Proceedings of the KAIS Fall Conference
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• 2006.05a
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• pp.599-601
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• 2006

본 논문에서는 용액의 농도가 이온교환 특성에 미치는 영향을 조사하기 위하여 농도는 $Na^+\;50$, 125, 250ppm, $Cl^-\;165$, 315, 610ppm, 입자성 물질의 유입 농도 0ppm, 유속 500ml/min, 이온교환 수지는 ROHM&HAAS IR 120 양이온 수지와 ROHM&HAAS IRA 402 음이온 수지를 사용하였다. 수지탑 배열은 혼상-혼상-음이온 수지탑 순으로, 이온교환 수지탑의 양 음이온교환 수지의 조성 비율은 1:2 로 실험한 결과 이온교환 수지탑 성능은 유입 용액 성분 및 농도에 영향을 받는 것으로 나타났다. 이온교환 수지탑 배열 순서에 따라 파과시점이 연장되며, 파과순서는 음이온의 경우 $Cl^-\;<\;NO_3\;^-\;<\;F^-$, 양이온의 경우 $Na^+\;<\;K^+\;<\;Ca^{2+}$ 순 이였으며, 용액의 농도가 증가할수록 파과시간이 단축되었다.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2006.11a
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• pp.153-155
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• 2006

메조포러스 탄소의 톨루엔 흡착은 peak가 사전실험을 거쳐 조사된 Reference에 도달함에 의해 파과되는 것을 확인하였다. pH와 촉매의 함량을 달리하여 제조한 메조포러스 탄소를 이용한 톨루엔의 흡착실험에서 MC50-6, MCl00-6, MC100-7, MC50-7의 순으로 파과됨을 나타내었다. 톨루엔 흡착에 효율적인 합성조건은 촉매보다는 pH에 따라 달리 제조된 메조포러스 카본이 우수함을 보여주었다.

• Journal of the Korean GEO-environmental Society
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• v.15 no.8
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• pp.39-44
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• 2014

Effects of operating parameters on the breakthrough properties of Pb(II) by $Mn_3O_4$ coated activated carbon prepared by supercritical technique were investigated through fixed-bed column experiments. The mass transfer zone and equilibrium adsorption capacity were enhanced about 2.8 times for Pb(II) by $Mn_3O_4$ coating onto activated carbon. Increase of bed height enhanced the residence time of Pb(II) in adsorption zone, giving the higher breakthrough time, mass transfer zone and equilibrium adsorption capacity. Increase of flow rate reduced the residence time and diffusion of Pb(II) in adsorption zone, therefore decreased the equilibrium adsorption capacity. The higher inlet concentration of Pb(II) decreased the breakthrough time and mass transfer zone through the promotion of Pb(II) transfer onto adsorbent.